|Veröffentlichungsdatum||7. Juli 2009|
|Eingetragen||26. Apr. 2007|
|Prioritätsdatum||11. Juni 2003|
|Auch veröffentlicht unter||US8357213, US20070189940, US20090304554|
|Veröffentlichungsnummer||11740349, 740349, US 7556660 B2, US 7556660B2, US-B2-7556660, US7556660 B2, US7556660B2|
|Erfinder||James Kevin Shurtleff, John Madison Patton, Eric J. Ladd|
|Ursprünglich Bevollmächtigter||James Kevin Shurtleff, John Madison Patton, Ladd Eric J|
|Zitat exportieren||BiBTeX, EndNote, RefMan|
|Patentzitate (107), Nichtpatentzitate (17), Referenziert von (16), Klassifizierungen (32), Juristische Ereignisse (3)|
|Externe Links: USPTO, USPTO-Zuordnung, Espacenet|
This application is CIP of Ser. No. 11/270,947 filed Nov. 12, 2005, now U.S. Pat. No. 7,438,732 and is a CIP of Ser. No. 10/459,991, filed Jun. 11, 2003 now U.S. Pat. No. 7,393,369.
1. Field of the Invention
The present invention relates to apparatuses and methods for producing hydrogen. The embodiments described herein relate to apparatuses and methods for releasing hydrogen from chemical hydrides.
2. Description of the Related Art
Various energy sources are used to fuel today's society. Fossil fuels such as coal, oil, and gas are some of the most commonly used fuels due to the comparatively large quantities available and minimal expense required to locate, collect, and refine the fossil fuels into usable energy sources. Alternative energy sources are available. Some of the alternative energy sources are readily available; however, the cost to generate, collect, or refine the alternative energy sources traditionally outweighs the benefits gained from the alternative energy sources.
Hydrogen is a plentiful alternative energy source; however, hydrogen generally exists as a molecule combined with one or more other elements. The additional elements add mass and may prevent the hydrogen from being a usable energy source. As a result, pure hydrogen is desired for use as an energy source. Pure hydrogen comprises free hydrogen atoms or molecules comprising only hydrogen atoms. Producing pure hydrogen using conventional methods is generally cost prohibitive.
Conventionally, pure hydrogen is generated by a chemical reaction which produces hydrogen molecules. One such chemical reaction occurs between water (H2O) and chemical hydrides. Chemical hydrides are molecules comprising hydrogen and one or more alkali or alkali-earth metals. Examples of chemical hydrides include lithium hydride (LiH), lithium tetrahydridoaluminate (LiAlH4), lithium tetrahydridoborate (LiBH4), sodium hydride (NaH), sodium tetrahydridoaluminate (NaAlH4), sodium tetrahydridoborate (NaBH4), and the like. The chemical hydrides produce large quantities of pure hydrogen when reacted with water, as shown in reaction 1.
Recently, the interest in hydrogen generation from chemical hydrides has increased, because of the development of lightweight, compact Proton Exchange Membrane (PEM) fuel cells. One by-product of the PEM fuel cells is water that can be used or reused to produce pure hydrogen from chemical hydrides for fuelling the PEM fuel cell. The combination of PEM fuel cells with a chemical hydride hydrogen generator offers advantages over other energy storage devices in terms of gravimetric and volumetric energy density.
Unfortunately, the prior art has encountered unresolved problems producing pure hydrogen from chemical water/hydride reactions. Specifically, conventional systems, methods, and apparatus have not successfully controlled the chemical reaction between the water and the chemical hydride without adversely affecting the gravimetric and volumetric energy density of the overall system.
The chemical reaction between water and chemical hydrides is very severe and highly exothermic. The combination of the water and the chemical hydride must be precisely controlled to prevent a runaway reaction or an explosion. Many attempts have been made to properly control the reaction while still preserving the gravimetric and volumetric energy density provided by the chemical hydrides
One attempt to properly control the reaction involves separating water from the chemical hydride using a membrane. Generally, the membrane passes water because of a difference in water pressure across the membrane. Water pressure on the side of the membrane opposite the chemical hydride pushes the water through the membrane. Other membranes utilize a capillary action to transport water from one side of the membrane to the other. Consequently, a water supply must be provided that supplies water to the water side of the membrane to be transported by capillary action to the chemical hydride side of the membrane.
Another unfortunate side effect of such a system is that often times the chemical or anhydrous hydride will “gum” or “clump” as water is introduced. Gumming or clumping refers to the spheres or other geometric shapes formed by the chemical hydride during the reaction. Water is able to react the outer portion of the “clump” to a certain depth, however, generally large portions of the “clump” remain unreacted because water does not penetrate deeply enough. Consequently, a large percentage of the chemical hydride can remain unreacted. This is unacceptable.
Accordingly, what is needed is an improved apparatus, system, and method that overcomes the problems and disadvantages of the prior art. The apparatus, system, and method should promote a substantially complete reaction of an anhydrous hydride reactant. In particular, the apparatus, system, and method should control a chemical reaction between water and a chemical hydride using a liquid permeable material without relying on a water pressure differential across the liquid permeable material. The liquid permeable material should allow substantially only water to pass. In addition, the apparatus, system, and method should control a chemical reaction between water and a chemical hydride using a liquid permeable material that functions to maintain a thin uniform distribution of anhydrous hydride within a reaction cartridge. Such an apparatus, system, and method are herein disclosed.
The present invention has been developed in response to the present state of the art, and in particular, in response to the problems and needs in the art that have not yet been fully solved by currently available hydrogen generation systems. Accordingly, the present invention has been developed to provide an apparatus, system, and method for promoting a substantially complete reaction of anhydrous hydride that overcome many or all of the above-discussed shortcomings in the art.
The apparatus is provided with a liquid permeable pouch that defines a cavity. A solid anhydrous hydride reactant is disposed within the cavity, the solid anhydrous hydride reactant having a permeation distance, and wherein the cavity comprises a cross-section such that each point within the cross-section is separated from a perimeter of the liquid permeable pouch by no more than double the permeation distance. The apparatus also includes a cartridge configured to receive the liquid permeable pouch and a liquid reactant such that at least a portion of the liquid permeable pouch is submerged in the liquid reactant.
In one embodiment, the permeation distance comprises a distance the liquid reactant is capable of traveling in reacted hydride. The apparatus may also include a plurality of tubular liquid permeable pouches connected in a side-by-side configuration. The cartridge may be cylindrical and be configured to receive a plurality of liquid permeable pouches that are rolled. The longitudinal axis of the spiral configuration may be oriented coaxial with a longitudinal axis of the cartridge. The plurality of liquid permeable pouches are disposed within the cartridge such that the plurality of liquid pouches form one or more liquid channels directing a flow of liquid reactant around the plurality of liquid permeable pouches in one embodiment of the apparatus.
In a further embodiment, the apparatus includes a plurality of liquid conduits radially spaced about a longitudinal axis of the cartridge, each liquid conduit positioned along side at least one tubular liquid permeable pouch. Furthermore, the cartridge is configured to receive a plurality of liquid permeable pouches having different lengths, the liquid permeable pouches stacked and arranged in alternating courses such that a course gap between two stacked liquid permeable pouches does not line up with the gap in an adjacent course of liquid permeable pouches.
The liquid permeable pouch may be formed substantially of a material having a maximum vertical wicking distance of about 0.3 inches per minute in a direction opposite a gravitational pull, and the liquid permeable pouch may be formed substantially of a material configured to maintain structural integrity through temperatures in the range of between about 5 degrees and about 200 degrees Celsius. In a further embodiment, the liquid permeable pouch is formed of a material configured to maintain structural integrity and contribute substantially no contaminates to the anhydrous hydride reactant during a reaction of the anhydrous hydride reactant.
The liquid permeable pouch, in one embodiment, comprises a material formed of a high percentage (at least 75%) polyester and low percentage (at most 25%) rayon which has some heat resistance. In another embodiment, the liquid permeable pouch comprises a material selected from the group consisting of a polymer material, a paper material, and a metal material. The liquid permeable pouch comprises a composite material comprising a combination of two of a polymer, paper, and metal in another embodiment.
In one embodiment, the liquid permeable pouch comprises a material that has a pore size below about 0.0025 inches, is chemically resistant in solutions between about pH 4 and about pH 13, and retains about 7.5 times the material's weight in water. Additionally, the liquid permeable pouch may comprise a pair of opposing walls joined by a pair of opposing longitudinal seams, the width of one wall between opposing longitudinal seams configured to maintain a thin uniform distribution of anhydrous hydride reactant within the cavity.
In one embodiment, the liquid permeable pouch has a width in the range of between about 0.25 inches and about 1.25 inches, and the permeation distance is selected in response to the liquid reactant permeability in the anhydrous hydride reactant. In a further embodiment, the permeation distance is about 0.25 inches. The apparatus also includes a liquid conduit configured to extend from a first end of the cartridge to a location near an opposing second end of the cartridge such that the cartridge is filled with the liquid reactant from the second end towards the first end. In another embodiment, a longitudinal axis of the cartridge is oriented in a vertical position. The longitudinal axis of the cartridge is oriented in a horizontal position in yet another embodiment.
The cartridge, in one embodiment, includes a first end, an opposing second end and an injection port located near the second end of the cartridge, such that the cartridge fills with the liquid reactant from the second end towards the first end. The apparatus may include a liner disposed on the interior of the cartridge, the liner configured to protect the interior of the cartridge from corrosion from the liquid reactant and anhydrous hydride reactant. In another embodiment, the apparatus includes a dry, powdered activating agent, the dry, powdered activating agent mixed with the solid, anhydrous hydride reactant to form a dry powder. In yet another embodiment, the cartridge has an internal pressure of about 30 psi.
The liquid permeable pouch provides for high energy density and efficient use of the anhydrous hydride reactant. Liquid reactant moved through the liquid conduit reacts with the anhydrous hydride reactant. The configuration of the liquid permeable pouch allows for a substantially complete reaction of the anhydrous hydride reactant in a controlled manner. Furthermore, the configuration of a plurality of liquid permeable pouch provides a consistent and uniform generation of hydrogen from the reaction of the anhydrous hydride reactant and the liquid reactant.
A system of the present invention is also presented. The system may include two rectangular sheets of liquid permeable material joined at their respective perimeters, the joined sheets having one or more seams that run from a long side of the sheets to an opposite long side of the sheets to form a plurality of liquid permeable containers. Each container has a cavity defined by opposite portions of the two sheets and the one or more seams. The cavity comprises a cross-section such that a point within the cross-section is separated from the sheets of the liquid permeable container by no more than double a permeation distance.
In one embodiment, an anhydrous hydride reactant may be disposed within the cavity of each liquid permeable container. The system also includes a cartridge configured to receive the liquid permeable containers and a liquid reactant such that at least a portion of the liquid permeable containers are submerged in the liquid reactant, the liquid permeable containers oriented substantially parallel to a longitudinal axis of the cartridge, and at least one liquid conduit extending into the cartridge. Each liquid permeable container may have a width between adjacent seams of about 0.75 inches, and the permeation distance is between 0.125 inches and 1 inch.
In a further embodiment, the plurality of liquid permeable containers is rolled from a short side of the sheets toward an opposite short side to form a spiral configuration. The longitudinal axis of the cartridge may be oriented in a vertical position in one embodiment. In another embodiment, the system includes a plurality of liquid conduits radially spaced in a spiral orientation about a longitudinal axis of the cartridge, each liquid conduit having a unique length. In yet another embodiment, the liquid permeable container distributes the liquid reactant by way of one of substantially woven strands and substantially of non-woven strands.
A method of the present invention is also presented. The method in the disclosed embodiments substantially includes the steps necessary to carry out the functions presented above with respect to the operation of the described apparatus and system. In one embodiment, the method includes joining two rectangular sheets of liquid permeable material at their respective perimeters, and forming one or more seals that extend from a long side of the sheets to an opposite long side to form a plurality of liquid permeable containers, each container having a cavity defined by opposite portions of the two sheets and at least one opening, each liquid permeable container having a cross-section configured such that a point within the cross-section is separated from a perimeter of the liquid permeable container by no more than double a permeation distance. The method also includes disposing an anhydrous hydride reactant within the cavity by way of the at least one opening, and sealing the at least one opening.
Reference throughout this specification to features, advantages, or similar language does not imply that all of the features and advantages that may be realized with the present invention should be or are in any single embodiment of the invention. Rather, language referring to the features and advantages is understood to mean that a specific feature, advantage, or characteristic described in connection with an embodiment is included in at least one embodiment of the present invention. Thus, discussion of the features and advantages, and similar language, throughout this specification may, but do not necessarily, refer to the same embodiment.
Furthermore, the described features, advantages, and characteristics of the invention may be combined in any suitable manner in one or more embodiments. One skilled in the relevant art will recognize that the invention may be practiced without one or more of the specific features or advantages of a particular embodiment. In other instances, additional features and advantages may be recognized in certain embodiments that may not be present in all embodiments of the invention.
These features and advantages of the present invention will become more fully apparent from the following description and appended claims, or may be learned by the practice of the invention as set forth hereinafter.
In order that the advantages of the invention will be readily understood, a more particular description of the invention briefly described above will be rendered by reference to specific embodiments that are illustrated in the appended drawings. Understanding that these drawings depict only typical embodiments of the invention and are not therefore to be considered to be limiting of its scope, the invention will be described and explained with additional specificity and detail through the use of the accompanying drawings, in which:
Reference throughout this specification to “one embodiment,” “an embodiment,” or similar language means that a particular feature, structure, or characteristic described in connection with the embodiment is included in at least one embodiment of the present invention. Thus, appearances of the phrases “in one embodiment,” “in an embodiment,” and similar language throughout this specification may, but do not necessarily, all refer to the same embodiment.
Furthermore, the described features, structures, or characteristics of the invention may be combined in any suitable manner in one or more embodiments. In the following description, numerous specific details are provided to give a thorough understanding of embodiments of the invention. One skilled in the relevant art will recognize, however, that the invention may be practiced without one or more of the specific details, or with other methods, components, materials, and so forth. In other instances, well-known structures, materials, or operations are not shown or described in detail to avoid obscuring aspects of the invention.
The housing 11 may include a first end 1 and an opposing second end 2. FIG. 1A's embodiment illustrates a rear end cap 12 at the opposing second end 2 of the housing 11 having a handle 13 allowing fuel cartridge 10 to be easily positioned and locked into place with other components of the overall hydrogen generation system as will be described below. In an alternate embodiment, the rear end cap 12 may be at the first end 1 of the housing 11.
The first end 1 of housing 11 opposite the opposing second end 2 and rear end cap 12 will comprise a front end cap 15 which is more clearly seen in
As best seen in
In one preferred embodiment, water injection tubes 30 will have an inside diameter ranging from about 0.5 to 5.0 mm with the inside diameter more preferably being about 1 mm. The injection tubes may be made of aluminum, brass, or other metal, PTFE, Nylon®, or other high temperature polymers. As suggested in
A further embodiment seen in
As suggested above, one embodiment of fuel cartridge 10 will contain a solid reactant such as an anhydrous chemical hydride. In certain embodiments, a chemical hydride may be considered a reducing compound containing a metal and hydrogen that generates hydrogen gas when it reacts with water or other oxidizing agents. Various examples of chemical hydrides are disclosed in U.S. application Ser. No. 10/459,991 filed Jun. 11, 2003 which is incorporated by reference herein. Nonlimiting examples of chemical hydrides may include sodium borohydride, lithium borohydride, lithium aluminum hydride, lithium hydride, sodium hydride, and calcium hydride.
In the embodiment seen in
In the embodiment of
Then the pouch 31 is rolled to a diameter sufficiently small to be inserted into tubular housing 11 as suggested in
Rolling the pouch 31 creates liquid channels 37 between adjacent portions of the rolled pouch 31 through which liquid may flow and surround the pouch 31 and sections 34 of the pouch 31. In one embodiment, water flows through the liquid channels 37 to surround sections 34 of the pouch 31 and permeates through the material of the pouch 31 to reach the reactant inside the sections 34 of the pouch 31. The liquid channels 37 direct the flow of liquid around the rolled pouch 31.
The water injection tubes 30 are then carefully inserted between overlapping layers of the rolled pouch 31.
A still further embodiment of cartridge 10 is seen in
In one embodiment, a plurality of hoses (not shown) will connect the plurality of water passages 46 (via hose fittings 53) in the receiver plate 40 to water passages 43, likewise equipped with hose fittings. In other embodiments, the passages 46 may connect directly to passages 43 through the internal volume of receiver plate 40, but forming long internal passages within receiver plate 40 adds substantial manufacturing complexity.
The receiver plate 40 seen in
In one embodiment of the present invention, the chemical hydride reactant utilized in the fuel cartridge may be a dry, powdered form of sodium borohydride (NaBH4) mixed with an activating agent. The NaBH4 is particularly suitable for use in the pouch 31 seen in
One effective activating material is magnesium chloride (MgCl2), since it is relatively lightweight, low cost, and strongly activating. Other potential activating agents are other salts of Group IIA (alkaline earth metals), or Group IIIA with Group VIIA (halides), such as AlCl3, BeF2, BeCl2, BeBr2, BeI2, MgF2, MgBr2, Mg2I, CaF2, CaCl2, CaBr2, and CaI2. The fluorides and chlorides are preferred because they have a lower molecular weight. However, some of these salts may be less preferred depending on their degree of solubility in water or if they are considered toxic (e.g., beryllium compounds).
Activating agents may also include other water soluble salts such as Group IA (alkali metals) salts including LiF, LiCl, LiBr, LiI, NaF, NaCl, NaBr, NaI, KF, KCl, KBr, and KI. Group IA and Group IIA hydroxides may be less preferred, since they make basic solutions in water and thus reduce the reaction rate. Group IA and Group IIA oxides may also be less preferred since they tend to be more stable and thus not as reactive. However, Group IA and Group IIA sulfides, sulfates, and selenides, such as Li2S, Li2Se, Mg(SO4)2 may be better activating agents if they are sufficiently water soluble. In one preferred embodiment, the activating agents will be from the group of MgCl2, BeCl2, LiCl, NaCl, or KCl. However, any of the above activating agents may be employed given the proper design and use conditions. In certain embodiments, the activating agent will have a grain size ranging from about mesh 10 to about mesh 1000.
In one preferred embodiment, the quantity of activating agent mixed with the chemical hydride will be from about 10 weight percent to about 65 weight percent and more preferably about 50 weight percent to about 60 weight percent. In one embodiment, the quantity of activating agent is 55 weight percent. In the embodiment where the solid reactant is 55 weight percent MgCl2, approximately 0.8 gm of water will be required to fully react each gm of solid reactant. One consideration in optimizing the amount of activating agent is determining the minimum amount of the material which gives the desired hydrogen generation rate and results in complete reaction/utilization of the NaBH4. For a 55 weight % MgCl2/NaBH4 mixture, the energy density is 3116 Whr/kg. For comparison, the energy density of a 20 weight % NaBH4/H2O mixture (i.e., NaBH4 dissolved in water) is 1066 Whr/kg, while the energy density for NaBH4 alone is 7101 Whr/kg.
An alternative activating agent may be an anhydrous or powdered acid such as boric acid (H3BO3), oxalic acid, tartaric acid, citric acid, etc. Such anhydrous acids can be mixed with the NaBH4 without reaction, but when water is added, the anhydrous acid dissolves and thus causes a reaction. Weak or relatively insoluble anhydrous acids such as boric acid when mixed with NaBH4 produce hydrogen in the presence of water at a relatively low rate, and thus are less preferred. Strong acids such as oxalic acid are very soluble in water and generate substantial hydrogen when mixed with NaBH4. However, this mixture is difficult to control and is also less preferred. However, intermediate strength acids, such as tartaric acid or citric acid are more favorable. In one preferred embodiment, the strength (Ka) of the dry acid will range from about 1×10−4 to about 1×10−11. In certain embodiments, the powdered acid will have a grain size ranging from about mesh 10 to about mesh 1000. In one preferred embodiment, the quantity of tartaric acid mixed with NaBH4 will be from about 5 to about 50 weight percent and more preferably about 8 to about 12 weight percent. In this embodiment, approximately 0.8 gm of water will be required to fully react each gram of solid reactant.
As a further alternative, an inexpensive, water-insoluble catalyst may be mixed with the NaBH4. The catalyst can act to accelerate the water/NaBH4 reaction as water is injected. Such metal catalyst could include Co, Ni, Cu, Pt, Pd, Fe, Ru, Mn, and Cr. Typically, the metal catalyst will be in a powder form (e.g., particles less than 25 um) and will be added to the chemical hydride in an amount of about 25 weight percent to about 65 weight percent. In this embodiment, approximately 0.8 gm of water will be required to fully react each gram of solid reactant.
A still further alternative to mixing an anhydrous activating agent with the NaBH4 may be to mix the water soluble activating agent in with the water before it is injected into the cartridge containing anhydrous NaBH4 or other metal hydride. This has the advantage that an aqueous substance such as hydrochloric acid (HCl) may be used. In this embodiment, the activating material is held in separate container or reservoir 60 such as seen in
Although NaBH4 is mainly discussed above, alternative chemical hydrides may include (but are not limited to) lithium borohydride, lithium aluminum hydride, lithium hydride, sodium hydride, and calcium hydride. In certain embodiments, these latter chemical hydrides need not be combined with a powdered activating agent as described above and may be activated with water alone.
Fuel cartridges such as those described above will typically be employed in a hydrogen generation system. One embodiment of such a hydrogen generation system is shown schematically in
Hydrogen gas exiting cartridge 10 will flow through a check valve 87 and a hydrogen filter/water trap 83 before being directed to a fuel cell or other device to which hydrogen is to be supplied. Filter/water trap 83 serves the dual purpose of filtering particulate out of the hydrogen and also removing excess moisture from the hydrogen gas. A water condenser/reservoir 85 will collect water from any moist air returned from the fuel cell or other hydrogen consuming device and will also store water collected from water trap 83 and transferred via transfer valve 84.
In operation, control system 75 will determine the volume of water to pump into fuel cartridge 10 based upon monitoring parameters such as the temperature of the chemical hydride (as indicated by temperature sensor 80) and the hydrogen pressure within the system as measured by pressure sensor 89. As hydrogen pressure drops below a predetermined level in system 1, water pump 78 will be activated to deliver water to fuel cartridge 10, thereby causing the chemical hydride in cartridge 10 to release additional hydrogen gas. The release of additional hydrogen gas will result in an increase of pressure in the system 1. In one embodiment, the fuel cartridge has an internal pressure that is maintained at a relative pressure above ambient of about 30 psi. The system 1 may maintain a pressure within a fuel cell of about 7 psi.
In one preferred embodiment, switching valves 77 will be individually controlled by control system 75 as described above. This allows pump 78 to deliver water through only one water injection tube 30 at a time and to sequentially deliver water to each injection tube 30. This sequential method of delivering water may in some instances provide a more uniform distribution of water than if all water injection tubes were simply manifolded together without individual control of water flow to each injection tube 30. Likewise, the temperature sensor 80 monitoring the temperature of the chemical hydride will allow control system 75 to make decisions regarding whether fans 81 should be turned on to cool cartridge 10 or whether water should be limited to slow down the reaction rate of the chemical hydride. Hydrogen generation system 1 may also include the cartridge sensor 82 which will signal control system 75 as to whether a fuel cartridge 10 is presently installed in the system and will also provide control system 75 with information concerning when a spent cartridge has been removed and a new, fully charged cartridge installed.
In another embodiment, a single injection tube 30 is used and the liquid reactant fills a vertical cartridge from the bottom up.
As hydrogen gas flows through filter/water trap 83, excess moisture in the hydrogen gas will be removed and when a sufficient amount of water has accumulated, will be transferred via transfer valve 84 to water condenser/reservoir 85. Hydrogen gas exiting filter/water trap 83 will be directed through line 90 to the particular hydrogen consuming device, which for illustrative purposes will be considered a fuel cell in the present description. Typically, a regulator 88 will be positioned in line 90 to assure the fuel cell is supplied with hydrogen at a constant pressure. If the hydrogen consuming device produces water vapor as a by-product (as do fuel cells), the moist air will be directed via line 86 back to condenser 85 and the water recovered from the air. Likewise, water vapor in the hydrogen passing through purge line 91 (another characteristic feature of fuel cells) will be recovered in condenser 85.
In another embodiment of the present invention, the injection switching valves 77 seen in
Suitable fabrics may include but are not limited to woven or nonwoven Nylon, Rayon, polyester, porous filter paper, or blends of these materials. In one embodiment, the material for the pouch 800 may be selected for optimal thickness, density, and water retention. In one embodiment, the cartridge (of
The water retention and wicking potential of the pouch 800 affect where the chemical reaction between the water and the chemical hydride occurs. Low water retention and wicking potential helps keep the chemical reaction at or below a water fill level in the cartridge. If the water retention and wicking potential are higher, the pouch 800 wicks and retains the water such that the chemical reaction can occur above the fill level of the cartridge. Selection of a material for the pouch 800 may be based on the configuration of the cartridge, the injection tubes, and the chemical hydride and activating agent in use, in order to more precisely control the chemical reaction within the cartridge.
Other relevant factors may include water permeability, porosity, chemical reactivity, and temperature stability between about 5° C. and about 200° C. relative to the chemical hydride, activating agent, and water injection system in use. A suitable thickness for the material for the pouch is between about 3 mils (0.003 inches) and 12 mils (0.012 inches). A suitable density is less than about 0.05 grams per square inch.
In one exemplary embodiment, the pouch 800 comprises Crane® 57-30, a product of Crane Nonwovens of Dalton, Mass. Crane® 57-30 has a thickness of about 0.0043 inches, has a density of about 57.9 grams per square meter, is water permeable, has a pore size below about 0.0025 inches, is chemically resistant in basic and acidic solutions of about pH 4 to about pH 13, is stable in temperatures up to about 180° C., and retains only about 7.5 times its own weight in water. Other combinations of material properties such as thickness, density, and water retention that are configured for stable hydrogen generation may also be used.
In one embodiment, the fabric pouch 800 is comparatively thin having a substantially greater width than thickness. The pouch 800 may be formed in any conventional manner. For example, two rectangular sheets of fabric material 802 and 804 may be sealed along three edges (for example by stitching or other sealing methods) and segmented into 0.25 to 1.25 inch wide sections to leave open ends 806 (See also
An illustrative width of the pouch 1400 (i.e., the distance between sealed edges 808 of sections when unrolled and charged with a chemical hydride) may be in the range of between about 0.25 and 1.25 inches. The plurality of pouches 800, in one embodiment may be rolled in a spiral configuration, as illustrated, in order to be inserted in to a tubular housing or cartridge. Alternatively, the pouches may in any configuration that promotes water channel distribution. The dimensions of the plurality of liquid permeable pouches 800 (hereinafter rolled pouch 810) may be determined based on the size of the cartridge, and the configuration of the pouch 800.
The water injection tubes may be inserted between layers of the rolled pouch 810. In one embodiment, the cartridge may be implemented in a vertical configuration in order to eliminate the need for injection tubes, as gravity will pull the liquid to the bottom of the cartridge and begin submerging the pouches and subsequently the anhydrous hydride. In another embodiment, a single injection tube receives injected liquid reactant and delivers the liquid reactant to the bottom of a vertical cartridge.
In one embodiment, a liner (not shown) is also disposed between the cartridge and the rolled pouch 810 in order to protect the cartridge from corrosion and damage. The liner may be removable or permanent, and may serve to extend the life of the cartridge. In one embodiment, the liner is a bag or pouch consisting of a plastic or other inert material known in the art, and the liner is configured to withstand the temperatures associated with a hydrogen generating chemical hydride reaction. One example of a liner is a polypropylene liner produced by Bradley Bags of Downey, Calif. Preferably, the liner is sized to be just smaller than the interior of the cartridge.
In one embodiment, the cartridge 900 is configured with 7 rolled pouches 810, as depicted, in an arrangement selected to maximize pouch density and therefore chemical hydride density. Of course the depicted embodiment is given by way of example only and the number of rolled pouches 810 may be increased or decreased depending upon the hydrogen requirements and dimensions of the system.
The liner 910, in one embodiment, is disposed between the cartridge 900 and the rolled pouches 810 in order to protect the cartridge 900 from corrosion and damage. The liner 910 may be removable or permanent, and may serve to extend the life of the cartridge 900. In one embodiment, the liner 910 is a bag or pouch consisting of a plastic or other inert material known in the art, and the liner 910 is configured to withstand the temperatures associated with a hydrogen generating chemical hydride reaction. One example of a liner 910 is a polypropylene liner produced by Bradley Bags of Downey, Calif. Preferably, the liner 910 is sized to be just smaller than the interior of the cartridge 900. As will be appreciated by one skilled in the art, the liner 910 may be in any configuration capable of protecting the cartridge 900 from corrosion, and may be employed when using multiple pouches 810 or a single pouch 810.
Offsetting the course gaps 1004 ensures that hydrogen production will be consistent while the pouches are being submerged during operation as the fill level of liquid reactant rises. For example, if the course gaps 1004 were aligned, when the fill level reached the course gap 1004 hydrogen production would slow until the subsequent stacked pouches 810 begin to be submerged. As depicted, the course gap 1004 a of course 1002 a may be aligned with the course gap 1004 c of course 1002 c however offset course gap 1004 b permits hydrogen production to continue. Alternatively, the lengths of the pouches 810 may be configured such that the two course gaps 1004 a and 1004 c do not align.
The material, as discussed above, may be selected from liquid permeable woven and non-woven fabrics. The term “liquid permeable,” as used herein, refers to a material that allows the passage of a selected liquid through mass transport mechanisms such as, but not limited to, diffusion due to a concentration, pressure, or temperature gradient. The sealed edges 808 form a plurality of cavities 1106 formed by the opposing sheets 1102, 1104 and separated by the sealed edges 808.
Typically a liquid causes a reaction at the surface of an anhydrous hydride when first contact is made. For example, hydrogen generation from borohydrides occurs initially when a water molecule contacts a particle of sodium borohydride. As the reaction continues, a layer of borate can form around a sodium borohydride core. This may be referred to as “encapsulation” or “gumming.” The reaction of the unreacted core depends on the ability of the liquid to penetrate or permeate through the reacted borate shell.
The permeation distance of the liquid depends on the type of liquid and anhydrous hydride selected for the hydrogen generation system. Other factors affecting the permeation distance are believed to include dry anhydrous hydride grain size, degree of compaction and settling of the anhydrous hydride, the temperature around the reaction, and the degree of vibration the system is expected to encounter. The permeation distance may also vary in response to the mol ratio between the anhydrous hydride and other components in the reaction, including the liquid reactant and the activating agent. Consequently, the width 1112 of the cavity is selected according to the permeation distance in order to maximize the efficiency of hydrogen production from the anhydrous hydride.
The present invention sizes the width 1112 of the pouches 800 such that the permeation distance is greater than the distance the liquid reactant must travel from the perimeter 1124 to reach a center point 1130 within the cross-section 1120. In embodiments in which the liquid reactant surrounds the pouch 800, the width 1112 of the pouches 800 is selected such that any point 1114, 1130 within the cross-sectional area of the cavity is at a distance of no more than twice the permeation distance from the perimeter 1124. In embodiments in which the liquid reactant contacts the pouch 800 on a single side, the width 1112 of the pouches 800 is selected such that a diameter of the cross-sectional area of the cavity is at a distance of no more than the permeation distance from the liquid reactant contacting side. In this manner, high energy density is provided within the pouch and little or no anhydride remains unreacted once the liquid reactant is provided.
The schematic flow chart diagrams that follow are generally set forth as logical flow chart diagrams. As such, the depicted order and labeled steps are indicative of one embodiment of the presented method. Other steps and methods may be conceived that are equivalent in function, logic, or effect to one or more steps, or portions thereof, of the illustrated method. Additionally, the format and symbols employed are provided to explain the logical steps of the method and are understood not to limit the scope of the method. Although various arrow types and line types may be employed in the flow chart diagrams, they are understood not to limit the scope of the corresponding method. Indeed, some arrows or other connectors may be used to indicate only the logical flow of the method. For instance, an arrow may indicate a waiting or monitoring period of unspecified duration between enumerated steps of the depicted method. Additionally, the order in which a particular method occurs may or may not strictly adhere to the order of the corresponding steps shown.
At this point the two sheets of liquid permeable material form a single pouch having a cavity for storing anhydrous hydride. The width of the two sheets may be selected to form a single pouch having a width 1112 in the range of between about 0.25 and 1.25 inches, or any width suitable for a desired permeation distance as described above. Alternatively, multiple pouches or cavities may be formed from the two sheets of liquid permeable material. The multiple pouches or containers may be formed 1206 by forming parallel seams within the two joined sheets 1102, 1104 to form a plurality of tubular pouches as illustrated in
The width between the seams is selected to maintain a thin uniform distribution of anhydrous hydride reactant in order to prevent gumming as described above with reference to
The method continues and an anhydrous hydride is disposed 1208 or deposited within the cavity of the liquid permeable container. Due to the selected width of the pouch, the anhydrous hydride is deposited in a thin uniform manner in order to prevent the forming of an impenetrable reacted shell. As such, a substantially complete reaction of anhydrous hydride is possible. Any openings may be sealed 1210 and the pouch rolled into a spiral configuration as shown in
The present invention may be embodied in other specific forms without departing from its spirit or essential characteristics. The described embodiments are to be considered in all respects only as illustrative and not restrictive. The scope of the invention is, therefore, indicated by the appended claims rather than by the foregoing description. All changes which come within the meaning and range of equivalency of the claims are to be embraced within their scope.
|US2542746||14. Nov. 1949||20. Febr. 1951||Metal Hydrides Inc||Method of purifying borohydrides of the alkali metals|
|US3133837||31. Dez. 1959||19. Mai 1964||Electric Storage Battery Co||Fuel cell system|
|US3313598||7. Juni 1965||11. Apr. 1967||Ethyl Corp||Method of controlled hydrogen generation|
|US3449078||24. Febr. 1967||10. Juni 1969||Shell Oil Co||Process for the preparation of hydrogen|
|US3511710||28. Juli 1965||12. Mai 1970||Varta Ag||Method of directly converting the chemical energy of complex hydrides into electrical energy|
|US3649360||16. Jan. 1970||14. März 1972||United Aircraft Corp||Combined water removal and hydrogen generation fuel cell powerplant|
|US3734863||11. Juni 1971||22. Mai 1973||Us Navy||Hydrogen generating compositions|
|US3940474||6. Aug. 1974||24. Febr. 1976||The United States Of America As Represented By The Secretary Of The Army||Generation of hydrogen|
|US3977990||30. Okt. 1974||31. Aug. 1976||The United States Of America As Represented By The Secretary Of The Navy||Controlled generation of cool hydrogen from solid mixtures|
|US4000003||2. Jan. 1976||28. Dez. 1976||The United States Of America As Represented By The Secretary Of The Army||Fuel cell-secondary cell combination|
|US4081345||30. Juli 1976||28. März 1978||Max-Planck-Gesellschaft Zur Foerderung Der Wissenschaften E.V.||Apparatus for determining small amounts of nitrogen|
|US4155712 *||6. Okt. 1977||22. Mai 1979||Taschek Walter G||Miniature hydrogen generator|
|US4261955||1. Sept. 1978||14. Apr. 1981||The United States Of America As Represented By The Secretary Of The Army||Vertical type porous membrane hydrogen generator|
|US4261956 *||13. Juni 1979||14. Apr. 1981||Engelhard Minerals & Chemicals Corporation||Cartridge for gas generator|
|US4433633||16. Apr. 1982||28. Febr. 1984||The United States Of America As Represented By The Secretary Of The Navy||Controlled gas generator system|
|US4436793||29. Sept. 1982||13. März 1984||Engelhard Corporation||Control system for hydrogen generators|
|US4463063||16. Juli 1982||31. Juli 1984||Engelhard Corporation||Hydrogen generator|
|US4463066||30. Sept. 1982||31. Juli 1984||Engelhard Corporation||Fuel cell and system for supplying electrolyte thereto|
|US4463068||30. Sept. 1982||31. Juli 1984||Engelhard Corporation||Fuel cell and system for supplying electrolyte thereto with wick feed|
|US4486276||24. Sept. 1981||4. Dez. 1984||Engelhard Corporation||Method for suppressing hydrogen formation in an electrolytic cell|
|US4513065||16. Mai 1984||23. Apr. 1985||Engelhard Corporation||Hydrogen generator|
|US4543246||4. Okt. 1984||24. Sept. 1985||Houser Clifford F||Hydrogen generator|
|US4628010||13. Dez. 1985||9. Dez. 1986||The United States Of America As Represented By The Secretary Of The Navy||Fuel cell with storable gas generator|
|US4740504||5. Febr. 1987||26. Apr. 1988||United States Borax & Chemical Corp.||Antihyperlipidemic amine boranes|
|US4782096||16. Sept. 1987||1. Nov. 1988||Foster Wheeler Usa Corporation||Process for the production of synthesis gas|
|US4940667||28. Dez. 1987||10. Juli 1990||Ionics, Incorporated||Apparatus for monitoring the quality of water|
|US4962462||26. Apr. 1989||9. Okt. 1990||Engelhard Corporation||Fuel cell/battery hybrid system|
|US4968393||18. Apr. 1988||6. Nov. 1990||A. L. Sandpiper Corporation||Membrane divided aqueous-nonaqueous system for electrochemical cells|
|US4973530||21. Dez. 1989||27. Nov. 1990||The United States Of America As Represented By The United States Department Of Energy||Fuel cell water transport|
|US4977094||23. Okt. 1989||11. Dez. 1990||Ionics, Incorporated||Process for monitoring the quality of water|
|US4978451||5. Sept. 1989||18. Dez. 1990||Separation Dynamics, Inc.||Supported hydrophilic membrane|
|US4988583||30. Aug. 1989||29. Jan. 1991||Her Majesty The Queen As Represented By The Minister Of National Defence Of Her Majesty's Canadian Government||Novel fuel cell fluid flow field plate|
|US5047301||3. Dez. 1990||10. Sept. 1991||Ergenics Power Systems, Inc.||High temperature battery and system utilizing same|
|US5108849||16. Aug. 1990||28. Apr. 1992||Her Majesty The Queen In Right Of Canada, As Represented By The Minister Of National Defence In Her Britannic Majesty's Government Of The United Kingdom Of Great Britain And Northern Ireland||Fuel cell fluid flow field plate|
|US5186903||27. Sept. 1991||16. Febr. 1993||North Carolina Center For Scientific Research, Inc.||Apparatus for treating indoor air|
|US5200278||15. März 1991||6. Apr. 1993||Ballard Power Systems, Inc.||Integrated fuel cell power generation system|
|US5205841||3. Apr. 1992||27. Apr. 1993||Tpc Technologies, Inc.||Apparatus and method for extracting hydrogen|
|US5221520||23. Okt. 1992||22. Juni 1993||North Carolina Center For Scientific Research, Inc.||Apparatus for treating indoor air|
|US5229222||12. Nov. 1991||20. Juli 1993||Sanyo Electric Co., Ltd.||Fuel cell system|
|US5264299||26. Dez. 1991||23. Nov. 1993||International Fuel Cells Corporation||Proton exchange membrane fuel cell support plate and an assembly including the same|
|US5292600||13. Aug. 1992||8. März 1994||H-Power Corp.||Hydrogen power cell|
|US5294410||1. Juni 1992||15. März 1994||Solar Turbine Incorporated||Gas purification and conditioning system|
|US5314762||30. Juni 1992||24. Mai 1994||Sanyo Electric Co., Ltd.||Portable power source|
|US5366820||12. Apr. 1993||22. Nov. 1994||Sanyo Electric Co., Ltd.||Fuel cell system|
|US5372617||28. Mai 1993||13. Dez. 1994||The Charles Stark Draper Laboratory, Inc.||Hydrogen generation by hydrolysis of hydrides for undersea vehicle fuel cell energy systems|
|US5382478||15. März 1994||17. Jan. 1995||Ballard Power Systems Inc.||Electrochemical fuel cell stack with humidification section located upstream from the electrochemically active section|
|US5514353||28. Juni 1994||7. Mai 1996||Af Sammer Corporation||Demand responsive hydrogen generator based on hydride water reaction|
|US5554343||9. Febr. 1995||10. Sept. 1996||Wade; Brian||Particle and light and heavy fluid separator|
|US5557188||1. Febr. 1994||17. Sept. 1996||Sun Microsystems, Inc.||Smart battery system and interface|
|US5593640||7. Juni 1995||14. Jan. 1997||Ball Corporation||Portable hydrogen generator|
|US5599640||17. Aug. 1995||4. Febr. 1997||Korea Advanced Institute Of Science And Technology||Alkaline fuel cell|
|US5634341||4. Dez. 1995||3. Juni 1997||The Penn State Research Foundation||System for generating hydrogen|
|US5683828||31. Okt. 1995||4. Nov. 1997||H Power Corp.||Metal platelet fuel cells production and operation methods|
|US5688611||1. Juli 1996||18. Nov. 1997||Ergenics, Inc.||Segmented hydride battery including an improved hydrogen storage means|
|US5702491||20. Sept. 1996||30. Dez. 1997||Ball Corporation||Portable hydrogen generator|
|US5728464 *||2. Jan. 1996||17. März 1998||Checketts; Jed H.||Hydrogen generation pelletized fuel|
|US5747189||22. Juli 1992||5. Mai 1998||Valence Technology, Inc.||Smart battery|
|US5756047||14. Dez. 1995||26. Mai 1998||Advanced Chemical Systems, Inc.||Air purification method|
|US5804329||28. Dez. 1995||8. Sept. 1998||National Patent Development Corporation||Electroconversion cell|
|US5833934 *||20. Dez. 1995||10. Nov. 1998||Af Sammer Corporation||Demand responsive hydrogen generator based on hydride water reaction|
|US5843297||23. Sept. 1996||1. Dez. 1998||Dornier Gmbh||Electrolysis process and apparatus|
|US5858587||16. Febr. 1996||12. Jan. 1999||Canon Kabushiki Kaisha||Positioning system and method and apparatus for device manufacture|
|US5861137||30. Okt. 1996||19. Jan. 1999||Edlund; David J.||Steam reformer with internal hydrogen purification|
|US5863671||17. Mai 1995||26. Jan. 1999||H Power Corporation||Plastic platelet fuel cells employing integrated fluid management|
|US5932365||9. Juni 1997||3. Aug. 1999||Industrial Technology Research Institute||Hydrogen canister fuel cell battery|
|US5948558||27. März 1997||7. Sept. 1999||National Patent Development Corporation||High energy density boride batteries|
|US5955039||19. Dez. 1996||21. Sept. 1999||Siemens Westinghouse Power Corporation||Coal gasification and hydrogen production system and method|
|US5962155||16. Jan. 1997||5. Okt. 1999||Matsushita Electric Industrial Co., Ltd.||Fuel cell system|
|US5976725||16. Juni 1997||2. Nov. 1999||Matsushita Electric Industrial Co., Ltd.||Fuel cell system, fuel feed system for fuel cell and portable electric appliance|
|US5996976||30. Apr. 1996||7. Dez. 1999||Lynntech, Inc.||Gas humidification system using water permeable membranes|
|US5997594||15. Okt. 1997||7. Dez. 1999||Northwest Power Systems, Llc||Steam reformer with internal hydrogen purification|
|US5997812||1. Aug. 1996||7. Dez. 1999||Coolant Treatment Systems, L.L.C.||Methods and apparatus for the application of combined fields to disinfect fluids|
|US6051128||6. Juni 1995||18. Apr. 2000||Chevron Chemical Company||Split-feed two-stage parallel aromatization for maximum para-xylene yield|
|US6051331||10. Okt. 1995||18. Apr. 2000||H Power Corporation||Fuel cell platelet separators having coordinate features|
|US6066409||16. Juli 1998||23. Mai 2000||Ballard Power Systems Inc.||Electrochemical fuel cell stack with improved reactant manifolding and sealing|
|US6072299||26. Jan. 1999||6. Juni 2000||Medtronic Physio-Control Manufacturing Corp.||Smart battery with maintenance and testing functions|
|US6090312||31. Jan. 1996||18. Juli 2000||Ziaka; Zoe D.||Reactor-membrane permeator process for hydrocarbon reforming and water gas-shift reactions|
|US6096219||12. Mai 1998||1. Aug. 2000||Sanitrol Systems, Inc.||Method and apparatus for pretreatment of hazardous waste material|
|US6096286||20. Okt. 1998||1. Aug. 2000||Dbb Fuel Cell Engines Gmbh||System for steam reformation of a hydrocarbon and operating method therefor|
|US6097175||25. Aug. 1998||1. Aug. 2000||Samsung Electronics Co., Ltd.||Method for charging and discharging a smart battery of an electronic equipment|
|US6106965||31. März 1997||22. Aug. 2000||Mazda Motor Corporation||Polymer electrolyte fuel cell|
|US6106968||6. März 1998||22. Aug. 2000||Lucent Technologies Inc.||Smart valve regulated lead acid battery with embedded electronic monitoring and fluid fill system|
|US6108968||30. Sept. 1998||29. Aug. 2000||Peng; Hai-Sung||Device for exterminating garden pests|
|US6110429||12. Nov. 1997||29. Aug. 2000||Johansing, Jr.; P. G.||Transformation of halogenated refrigerant gases|
|US6110611||1. Apr. 1999||29. Aug. 2000||Siemens Aktiengesellschaft||Process for operation of a PEM fuel cell unit|
|US6156450||24. Juli 1997||5. Dez. 2000||Eveready Battery Company, Inc.||Battery tester having printed electronic components|
|US6198253||23. Dez. 1999||6. März 2001||Medtronic Physio-Control Manufacturing Corp.||Smart battery with maintenance and testing functions, communications, and display|
|US6221117||13. Apr. 1999||24. Apr. 2001||Idatech, Llc||Hydrogen producing fuel processing system|
|US6231825||29. Juli 1999||15. Mai 2001||Rohm And Haas Company||Production of sodium borohydride from sodium borohydride dihydrate in a fluidized bed dryer|
|US6236326||29. Okt. 1999||22. Mai 2001||Vtech Telecommunications, Ltd.||Method and apparatus for intelligently signaling a battery charge condition in a wireless telephone|
|US6238814||18. Dez. 1998||29. Mai 2001||Kabushikikaisha Equos Research||Fuel cell system|
|US6248469||3. März 1999||19. Juni 2001||Foster-Miller, Inc.||Composite solid polymer electrolyte membranes|
|US6250078||27. Apr. 2000||26. Juni 2001||Millennium Cell, L.L.P.||Engine cycle and fuels for same|
|US6268077||1. März 1999||31. Juli 2001||Motorola, Inc.||Portable fuel cell power supply|
|US6274093||6. Aug. 1998||14. Aug. 2001||Ball Aerospace & Technologies Corp.||Self-regulating hydrogen generator|
|US6309611||8. Apr. 1999||30. Okt. 2001||University Of Central Florida||Apparatus for low flux photocatalytic pollution control|
|US6312848||13. Dez. 1999||6. Nov. 2001||Varta Geratebatterie Gmbh||Electrical rechargeable battery in the form of a button cell|
|US6315870||8. Apr. 1999||13. Nov. 2001||University Of Central Florida||Method for high flux photocatalytic pollution control|
|US6334936||10. Apr. 1999||1. Jan. 2002||University Of Central Florida||Method for decoupled thermo-catalytic pollution control|
|US6337120||24. Juni 1999||8. Jan. 2002||Nok Corporation||Gasket for layer-built fuel cells and method for making the same|
|US6342128||10. Apr. 1999||29. Jan. 2002||University Of Central Florida||Method and apparatus for decoupled thermo-photocatalytic pollution control|
|US6387557||20. Sept. 2000||14. Mai 2002||Utc Fuel Cells, Llc||Bonded fuel cell stack assemblies|
|US6399234||13. Dez. 2000||4. Juni 2002||Utc Fuel Cells, Llc||Fuel cell stack assembly with edge seal|
|US6544400 *||30. März 2001||8. Apr. 2003||Manhattan Scientifics, Inc.||Portable chemical hydrogen hydride system|
|US6746496 *||9. Juli 2002||8. Juni 2004||Sandia Corporation||Compact solid source of hydrogen gas|
|US7083657 *||20. Aug. 2002||1. Aug. 2006||Millennium Cell, Inc.||System for hydrogen generation|
|US7097813 *||21. Juni 2002||29. Aug. 2006||Hewlett-Packard Development Company, L.P.||Hydrogen generating apparatus|
|1||"A Novel High Power Density Borohydride-Air Cell," Amendola S.C. et al., Journal of Power Sources, vol. 84, No. 1, Nov. 1999, pp. 130-133(4).|
|2||"A safe, portable, hydrogen gas generator using aqueous borohydride solution and Ru catalyst" Amendola, S.C. et al., International Journal of Hydrogen Energy 25 (2000) 969-975.|
|3||"Catalytic Reformer and Refinery Hydrogen System," Pall Corporation Copyright 1996, East Hills, New York.|
|4||"Dollinger Hydrogen Purification System," B & H Dollinger Filters, May 8, 2008, http://www.bhindust.com/dollinger/Dollinger-Hydrogen-Purification-System.htm.|
|5||"Enabling Fuel Cells for Standby Power-Chemical Hydride Fueling Technology," Smith, G.M., et al. Millennium Cell Inc., Eatontown, Telecommunications Energy Conference, 2004, Sep. 19-23, 2004.|
|6||"Fuel Chemistry News" Newsletter of the ACS Division of Fuel Chemistry, vol. 82, No. 2, Fall 2003.|
|7||"Hydrogn Generation Via Sodium Borohydride," Mohring, R.M., et al. Millennium Cell, Inc., Eatontown, AIP Conference Proceedings-Jul. 11, 2003-vol. 671, Issue 1, pp. 90-100.|
|8||"Recent Advances in Hydrogen Storage in Metal-Containing Inorgainc Nanostructures and Related Materials," Seayad, A.M., et al. Copyright 2004 May 19, 2004.|
|9||"Recovery and Purification of Hydrogen Using PSA Technology," NATCO, May 8, 2008, http://www.natcogroup.com/Content.asp?t=ProductPage&ProductID=70.|
|10||"Review of Chemical Processes for the Synthesis of Sodium Borohydride" Wo, Y. et al., Millennium Cell Inc., Aug. 2004.|
|11||"Solid Storage," Luzader, R., Millennium Cell, Inc., Eatontown, News, Jun./Jul. 2003.|
|12||"VI.B.4 DOE Chemical Hydrogen Storage Center of Excellence" Tumas, W. et al., FY 2005 Progress Report.|
|13||"Will Fuel Cells Replace Batteries in Mobile Devices?" Paulson, L.D. Millennium Cell, Inc. Eatontown, News, Nov. 2003.|
|14||Amendola et al., "A Safe, Portable, Hydrogen Gas Generator Using Aqueous Borohydride Solution and Ru Catalyst", International Journal of Hydrogen Energy, 2000, 25, pp. 969-975.|
|15||Eatontown, NEWS, Nov. 2003.|
|16||Messina-Boyer, Chris. "Millennium Cell Receives Patent on System for Hydrogen Generation," Millennium Cell, Inc., Eatontown, News, Mar. 18, 2003.|
|17||QuestAir H-3200: Hydrogen Purification PSA System, QuestAir Technologies, British Columbia, Canada 2008.|
|Zitiert von Patent||Eingetragen||Veröffentlichungsdatum||Antragsteller||Titel|
|US7807131 *||1. Nov. 2007||5. Okt. 2010||Honeywell International Inc.||Hydrogen producing fuel for power generator|
|US8152873 *||22. Dez. 2009||10. Apr. 2012||Trulite, Inc||System for generating hydrogen from a chemical hydride|
|US8187348||9. März 2009||29. Mai 2012||Honeywell International Inc.||Hydrogen generator|
|US8337806||8. Juni 2010||25. Dez. 2012||Honeywell International Inc.||Hydrogen producing fuel for power generator|
|US8551663||25. Apr. 2007||8. Okt. 2013||Honeywell International Inc.||Power generator with additional hydrogen storage|
|US8993135||1. Nov. 2007||31. März 2015||Honeywell International Inc.||Fuel cell stack for hydrogen fuel power generator|
|US9029038||1. Nov. 2007||12. Mai 2015||Honeywell International Inc.||Method of forming a fuel cell stack|
|US9061908 *||2. Nov. 2012||23. Juni 2015||Young Green Energy Co.||Hydrogen-generating device|
|US9225027||27. März 2015||29. Dez. 2015||Honeywell International Inc.||Method of forming a fuel cell stack|
|US20080268303 *||25. Apr. 2007||30. Okt. 2008||Honeywell International, Inc.||Power generator with additional hydrogen storage|
|US20090113795 *||1. Nov. 2007||7. Mai 2009||Honeywell International Inc.||Hydrogen producing fuel for power generator|
|US20090117442 *||1. Nov. 2007||7. Mai 2009||Honeywell International Inc.||Method of forming a fuel cell stack|
|US20090252670 *||9. März 2009||8. Okt. 2009||Honeywell International Inc.||Hydrogen generator|
|US20100129266 *||22. Dez. 2009||27. Mai 2010||Trulite Inc.||System for generating hydrogen from a chemical hydride|
|US20100247750 *||8. Juni 2010||30. Sept. 2010||Honeywell International Inc.||Hydrogen producing fuel for power generator|
|US20130115142 *||2. Nov. 2012||9. Mai 2013||Po-Kuei Chou||Hydrogen-generating device|
|US-Klassifikation||48/61, 48/174, 422/236, 422/234, 422/239, 48/120, 422/211|
|Internationale Klassifikation||C01B3/26, C10J3/20, H01M8/06|
|Unternehmensklassifikation||B01J2208/00539, B01J2219/002, C01B2203/066, H01M8/065, B01J8/0271, B01J2208/00017, H01M8/04216, Y02E60/50, B01J7/02, Y02E60/362, H01M8/04208, B01J2219/00231, B01J2219/00213, F17C11/005, C01B3/065|
|Europäische Klassifikation||C01B3/06C, F17C11/00D, H01M8/06B4, H01M8/04C6B, H01M8/04C6D, B01J7/02, B01J8/02D6|
|10. Juli 2012||FPAY||Fee payment|
Year of fee payment: 4
|24. Febr. 2014||AS||Assignment|
Free format text: JUDGMENT;ASSIGNOR:TRULITE, INC.;REEL/FRAME:032331/0605
Effective date: 20140218
Owner name: ALONSO, MOLLY, TEXAS
|18. März 2014||AS||Assignment|
Owner name: MCCLAREN ADVANCE, L.P., TEXAS
Effective date: 20100623
Free format text: SECURITY INTEREST;ASSIGNOR:TRULITE, INC.;REEL/FRAME:032460/0482
Effective date: 20101203
Free format text: SECURITY INTEREST;ASSIGNOR:TRULITE, INC.;REEL/FRAME:032460/0523
Owner name: MCCLAREN ADVANCE, L.P., TEXAS